Natural Gas Density & Sp. Volume Calculation

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  • 7/21/2019 Natural Gas Density & Sp. Volume Calculation

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    A Computation

    A.1 Computation of Molar Weight & Specific Volume of Gas

    A.1.1 Moler weight of Fuel gas composition

    Molecular

    weight (M)

    Mole %

    (F)

    Moler

    weight

    (gm) (M

    X F)

    Nitrogen (N2) 28 1.4 40.2

    Methane (CH4) 16 91.7 1467.0

    Ethane (C2H6) 30 4.5 135.0

    Propane (C3H8) 44 0.8 33.0

    Butane (C4H10) 58 0.3 15.5

    Pentane (C5H12) 72 0.1 5.7

    Total weight of 98.7 mole = 1696.4 gm

    Molar weight of gas = 17.18361 gm

    (For molecular weight of individual constituent of gas, Refer Attachment)

    Specific gravity of the gas = Molar weight of gas / 28.95

    = 0.5936

    A.1.2 Specific volume of Fuel gasSpecific volume of gas =

    Molar weight of gas

    where 22.4 litre is the molar volume of any gas a

    = 22.4 / 17.184

    = 1.3036 m3/kg at NTP

    Pressure P1 = 0 bar g

    Temperature T1 = 0

    o

    CSpecific volume V1 = 1.3036 Nm

    3/kg

    Pressure P2 = 3.5 bar g

    Temperature T2 = 60oC

    Specific volume V2 = 0.35697879 m3/kg

    Pressure P1 = 0 bar g

    Temperature T1 = 0oC

    NTP

    Per design basis 2.3, the composition of natural gas along with the computation of mola

    Composition

    22.4

    Aux. Boiler

    NTP

    condition

    Acutal

    Condition

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    Specific volume V1 = 1.3036 Nm3/kg

    Pressure P2 = 45.1 bar g

    Temperature T2 = 60oC

    Specific volume V2 = 0.034938646 m3/kg

    As per Ideal gas equation, for a fixed quantity of gas

    V2 = P1 X V1 X T2 T1 X P2

    Pressure P2 = 0 bar g

    Temperature T2 = 15oC

    Specific volume V2 = 1.375192346 m3/kg

    Calorific Valve of Fuel Gas CV = 800 Btu/scf

    17622.79341 Btu/lb

    Auxiliary Boiler Sizing

    Fuel Gas Parameters :

    Fuel Gas Terminal Pressure 3.5 Bar,g

    Fuel Gas Terminal Temperature 60 Deg.C

    Fuel Gas Specific Volume (Operating Condition) 0.3570 m3/kg

    Fuel Gas Specific Volume (Standard Condition) 1.3752 m3/kg

    Fuel Gas Enthalpy 800 Btu/scf

    17622.8 Btu/lbs

    Aux Boiler Heat Load 15368305.5 Btu/hr From Anti I

    Fuel Gas flow rate required 1014.0 lb/hr

    550.0 kg/hr

    196.3 m3/hr

    Considering 10% margin on flow 216 m3/hr

    Gas Turbine Sizing

    Fuel Gas Parameters :

    Fuel Gas Terminal Pressure 45.1 Bar,g

    Fuel Gas Terminal Temperature 60 Deg.C

    Fuel Gas Specific Volume (Operating Condition) 0.0349 m3/kg

    Fuel Gas Specific Volume (Standard Condition) 1.3036 m3/kg

    Fuel Gas Enthalpy 800 Btu/scf

    16704.9 Btu/lbs

    Gas

    Turbine

    Acutal

    Condition

    STP

    Condition

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    Aux Boiler Heat Load 430000000.0 Btu/hr From Gas T

    Fuel Gas flow rate required 29931.3 lb/hr

    14950.0 kg/hr

    522.3 m3/hr

    Considering 10% margin on flow 575 m3/hr

    453.674

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    t NTP.

    weight is as under.

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    cing Calculation

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    urbine Data